DK155835B - PROCEDURE FOR THE FUEL PREPARATION CONSISTS OF A MIXTURE OF SOLID BIOMASS AND FAT AND / OR OIL SLUDGE CONCENTRATIONS - Google Patents

PROCEDURE FOR THE FUEL PREPARATION CONSISTS OF A MIXTURE OF SOLID BIOMASS AND FAT AND / OR OIL SLUDGE CONCENTRATIONS Download PDF

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Publication number
DK155835B
DK155835B DK472485A DK472485A DK155835B DK 155835 B DK155835 B DK 155835B DK 472485 A DK472485 A DK 472485A DK 472485 A DK472485 A DK 472485A DK 155835 B DK155835 B DK 155835B
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DK
Denmark
Prior art keywords
fuel
fat
sludge
mixture
straw
Prior art date
Application number
DK472485A
Other languages
Danish (da)
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DK472485D0 (en
DK472485A (en
DK155835C (en
Inventor
Peter Saxberg
Original Assignee
Danergi As
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Danergi As filed Critical Danergi As
Publication of DK472485D0 publication Critical patent/DK472485D0/en
Priority to DK472485A priority Critical patent/DK155835C/en
Priority to PCT/DK1986/000112 priority patent/WO1987002377A1/en
Priority to JP61505646A priority patent/JP2550333B2/en
Priority to BR8606939A priority patent/BR8606939A/en
Priority to AT86906294T priority patent/ATE70853T1/en
Priority to DE8686906294T priority patent/DE3683156D1/en
Priority to EP86906294A priority patent/EP0252924B1/en
Priority to AU64797/86A priority patent/AU6479786A/en
Publication of DK472485A publication Critical patent/DK472485A/en
Priority to NO872438A priority patent/NO170226C/en
Priority to FI872657A priority patent/FI85873C/en
Publication of DK155835B publication Critical patent/DK155835B/en
Application granted granted Critical
Publication of DK155835C publication Critical patent/DK155835C/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Treatment Of Sludge (AREA)
  • Fats And Perfumes (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Fuel Cell (AREA)

Abstract

A fuel consists of a mixture of 26-72% cellullosic fibres like straw and sugar-cane fibres and 26-74% fat- and/or oilcontaining sludges from slaughter-houses, milk-condensation plants, fishing industry, distilleries, public dry-cleaning establishments and tanker transports. The water content in the sludge is preferably 50%. The fat- and/or oilcontaining sludge is heated to about 15-40<o>C, after which the sludge is mechanically admixed with the cellullosic fibres, after which the fuel is immediately ready for use. A fuel analysis indicates an upper caloric value of 3920 Kcal/kg for a mixture with a straw to sludge ratio of 1:1. In addition to its value as fuel you avoid oil- and/or fatcontamination in the environment.

Description

DK 155835 BDK 155835 B

Opfindelsen angår en fremgangsmåde til fremstilling af brændsel bestående af en blanding af fast biomasse såsom halmstrå, sukkerrørsfibre, papir og træflis samt fedt-og/eller olieholdige slamkoncentrationer fra slagterier, 5 mælkekondenseringsfabrikker, fiskeindustrien, destillerier, offentlige rensningsanlæg eller tankskibstransporter, hvor slamkoncentrationerne rent mekanisk blandes med den faste biomasse i et sådan forhold, at det færdige brændsel har et tørstofindhold på 40-80% fortrinsvis 60% og et vandinhold 10 på 20-60% fortrinsvis 40%.The invention relates to a process for the production of fuel consisting of a mixture of solid biomass such as straw, sugar cane fibers, paper and wood chips, and fat and / or oil-containing sludge concentrations from slaughterhouses, milk condensing plants, the fishing industry, distilleries, public purification plants or tanker plants. is mixed with the solid biomass in such a ratio that the finished fuel has a solids content of 40-80% preferably 60% and a water content 10 of 20-60% preferably 40%.

En række industrier og rensningsanlæg udleder henholdsvis opsamler store mængder olie- og/eller fedtholdige slamkoncentrationer. En del af slammet deponeres på lossepladser, 15 og en del udledes til vandig recipient. Den olie- og/eller fedtholdige slamkoncentration repræsenterer en brændselsmængde, som ikke nyttiggøres i dag, men er en miljøbelastende faktor på den måde, som man udleder og deponerer slamkoncentrationerne i dag. Opfindelsen tager sigte på at 20 anvise en løsning på, hvorledes de olie og/eller fedtholdige slamkoncentrationer kan anvendes som brændsel og uden at overføre miljøbelastningen til den luftformige recipient.A number of industries and wastewater treatment plants, respectively, collect large amounts of oil and / or greasy sludge concentrations. Part of the sludge is deposited at landfills, 15 and part discharged into aqueous recipient. The oil and / or fat-containing sludge concentration represents a quantity of fuel that is not recovered today, but is an environmentally damaging factor in the way in which the sludge concentrations are discharged and deposited today. The invention aims to provide a solution to how the oil and / or greasy sludge concentrations can be used as fuel and without transferring the environmental load to the gaseous recipient.

Fra dansk fremlæggelsesskrift nr. 148 119 kendes der en 25 fremgangsmåde til fremstilling af halmbriketter, hvor der før presningen tilsættes vandholdigt slam fra mindre rensningsanlæg med slambed, der indeholder organisk materiale til halmen. Fremgangsmåden omhandlet i dette fremlæggelses-skrift er baseret på den kendsgerning, at der sker en stor 30 varmeudvikling i briketterne under presningen. Varmeudviklingen er så stor, at der sker en delvis fordampning af slammets vandindhold. På trods af denne fordampning kan der kun anvendes en slamtilsætning på 10-25% med et vandindhold på mellem 25-35% efter soltørring af slammet. I et eksempel 35 refereret i fremlæggelsesskriftet angives den øvre brændværdi til 16495 kcal/kg for en prøve med ca. 17% slam medDanish Patent Specification No. 148,119 discloses a method of making straw briquettes in which prior to pressing, aqueous sludge is added from smaller sewage treatment plants containing organic matter to the straw. The method of this disclosure is based on the fact that there is a large heat development in the briquettes during pressing. The heat generation is so great that a partial evaporation of the water content of the sludge takes place. Despite this evaporation, only a sludge addition of 10-25% with a water content of between 25-35% after solar drying of the sludge can be used. In an example 35 referenced in the disclosure, the upper calorific value is stated to be 16495 kcal / kg for a sample of approx. 17% sludge included

DK 155835 BDK 155835 B

2 et vandindhold på ca. 30%.2 has a water content of approx. 30%.

Formålet med opfindelsen er således at angive en fremgangsmåde til fremstilling af et brændsel af den indledningsvis 5 angivne art, hvor man kan anvende en større tilsætning af olie- og/eller slamkoncentration og et større vandindhold end hidtil kendt. Samtidig skal brændslet kunne fremstilles på enkel vis uden investering i dyrt, energikrævende og kapacitetsbegrænsende maskineri som en briketteringspresse.The object of the invention is thus to provide a process for the production of a fuel of the type mentioned in the preamble, where a greater addition of oil and / or sludge concentration and a greater water content than previously known can be used. At the same time, the fuel must be able to be manufactured in a simple way without investing in expensive, energy-intensive and capacity-limiting machinery as a briquetting press.

10 Dette opnås ifølge opfindelsen ved, at den fedt- og/eller olieholdige slamkoncentration varmes op til ca. 15-40°C før blandingen, og efter blandingen er brændslet umiddelbart klar til afbrænding.This is achieved according to the invention by heating the fat and / or oily sludge concentration to approx. 15-40 ° C before mixing and after mixing the fuel is ready for burning immediately.

15 Det har overraskende vist sig, at man ved en simpel mekanisk blanding af den fedt- og/eller olieholdige slamkoncentration og cellulosefibrene efter en forudgående opvarmning af slamkoncentrationen til 25-35°C, hvor den bliver en homogen flydende masse, kan tilsætte væsentligt større mæng-20 der slamkoncentration med højere vandindhold og opnå gode resultater for brændværdien. Brændslets blandingsforhold efter vægt er typisk 26-74% halm og 74-26% olie- og/eller fedtkoncentration, hensigtsmæssigt er blandingsforholdet 1:1. En typisk slam indeholder 85% vand og 15% olie og/el-25 ler fedt og i afdrænet tilstand 40%vand og 60% olie og/eller fedt.Surprisingly, it has been found that by a simple mechanical mixture of the fat and / or oily mud concentration and the cellulose fibers, after a previous heating of the mud concentration to 25-35 ° C, where it becomes a homogeneous liquid mass, it is possible to add substantially greater amounts of sludge concentration with higher water content and obtain good results for the calorific value. The fuel ratio by weight is typically 26-74% straw and 74-26% oil and / or fat concentration, preferably the ratio is 1: 1. A typical slurry contains 85% water and 15% oil and / or 25 grease and in the drained state 40% water and 60% oil and / or grease.

Ved et forsøg blev en fedtslamkoncentration med et vandindhold på ca. 50% vægtprocent opvarmet til ca. 30°C. Slammet 30 blev blandet med halm i forholdet 1:1, hvorved halmens volumen formindskedes væsentligt. Det viser sig, at fedtslammet ved blandingen fordeler sig på stråenes overflade. Blandingen var lugtfri og straks brændbar i fyringsanlæg for brændsler med højt indhold af flygtige bestanddele. En 35 brændselsanalyse viser en øvre brændværdig på 16412 kcal/kg. Tørstofindholdet var 61,5% og askeindholdet 5,3% 3In one experiment, a fat sludge concentration with a water content of approx. 50% by weight heated to approx. 30 ° C. The sludge 30 was mixed with straw in a 1: 1 ratio, thereby significantly reducing the volume of the straw. It turns out that the fat mud in the mixture is distributed on the surface of the straw. The mixture was odorless and immediately flammable in combustion plants for high volatile fuel fuels. A 35 fuel analysis shows an upper calorific value of 16412 kcal / kg. The solids content was 61.5% and the ash content 5.3% 3

DK 155835BDK 155835B

T.S.T. S.

I et andet forsøg blandes 500 kg fiskeslam med 70% vand efter opvarmning med 500 kg byghalm med 9-11% vand. Ved af-5 brændingen var blandingens vandindhold 42,1%. Brændselsanalysen viser en øvre brændværdi på 14440 kJ/kg. Askeindholdet var 1,5%.In another experiment, 500 kg of fish sludge is mixed with 70% water after heating with 500 kg of barley straw with 9-11% water. At the firing, the water content of the mixture was 42.1%. The fuel analysis shows an upper calorific value of 14440 kJ / kg. The ash content was 1.5%.

Ved et tredie forsøg blandes 500 kg slagterislam med 60% 10 vand efter opvarmning med 500 kg byghalm med 9-11% vand.In a third experiment, 500 kg of butcher's sludge is mixed with 60% 10 water after heating with 500 kg of barley straw with 9-11% water.

Ved afbrændingen var blandingens vandindhold 48,2%. Brændselsanalysen viste en øvre brændværdi på 11980 kJ/kg. Askeindholdet var 1,8%.At burning, the water content of the mixture was 48.2%. The fuel analysis showed an upper calorific value of 11980 kJ / kg. The ash content was 1.8%.

15 Resultatet af blandingen er således, at man får 2 kg brændsel for hvert kg halm med et energiindhold svarende til 2 kg halm og med et betydeligt lavere volumen. Det lige så væsentlige og om ikke mere væsentlige er, at man slipper af med de forurenende olie- og/eller fedtkoncentrationer i 20 miljøet.The result of the mixture is such that one gets 2 kg of fuel for each kg of straw with an energy content corresponding to 2 kg of straw and with a considerably lower volume. Equally important and if not more important is that you get rid of the polluting oil and / or fat concentrations in the environment.

Claims (1)

DK 155835B Fremgangsmåde til fremstilling af brændsel bestående af en blanding af fast biomasse såsom halmstrå, sukkerrørsfibre, 5 papir og træflis samt f^dt- og/eller olieholdige slamkoncentrationer fra slagterier, mælkekondenseringsfabrikker, fiskeindustrien, destillerier, offentlige rensningsanlæg eller tankskibstransporter, hvor slamkoncentrationerne rent mekanisk blandes med den faste biomasse i et sådan forhold, 10 at det færdige brændsel har et tørstofindhold på 40-80% fortrinsvis 60% og et vandinhold på 20-60% fortrinsvis 40% kendetegnet ved, at den fedt- og/eller olieholdige slamkoncentration varmes op til ca. 15-40°C før blandingen, og at umiddelbart efter blandingen er brændslet 15 klar til afbrænding.DK 155835B Process for the production of fuel consisting of a mixture of solid biomass such as straw, sugar cane fiber, 5 paper and wood chips, as well as mud and / or oil-containing sludge concentrations from slaughterhouses, milk condensation factories, fish industry, distilleries, public purification plants or public purification plants, mechanically mixed with the solid biomass in such a ratio that the finished fuel has a solids content of 40-80% preferably 60% and a water content of 20-60% preferably 40%, characterized in that the fat and / or oily sludge concentration heated to approx. 15-40 ° C before mixing and that immediately after mixing, fuel 15 is ready for burning.
DK472485A 1985-10-16 1985-10-16 PROCEDURE FOR THE FUEL PREPARATION CONSISTS OF A MIXTURE OF SOLID BIOMASS AND FAT AND / OR OIL SLUDGE CONCENTRATIONS DK155835C (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
DK472485A DK155835C (en) 1985-10-16 1985-10-16 PROCEDURE FOR THE FUEL PREPARATION CONSISTS OF A MIXTURE OF SOLID BIOMASS AND FAT AND / OR OIL SLUDGE CONCENTRATIONS
JP61505646A JP2550333B2 (en) 1985-10-16 1986-10-09 Method for producing fuel using sludge or waste containing at least one of fat and oil
PCT/DK1986/000112 WO1987002377A1 (en) 1985-10-16 1986-10-09 Fuel consisting of a mixture of cellulosic fibres and fat- and/or oilcontaining sludges or waste materials
BR8606939A BR8606939A (en) 1985-10-16 1986-10-09 FUEL CONSISTING OF A MIXTURE OF CELLULOSIC FIBERS AND SLUDGE OR RESIDUAL MATERIALS CONTAINING FAT AND / OR OIL
AT86906294T ATE70853T1 (en) 1985-10-16 1986-10-09 USE AS FUEL OF A MIXTURE OF CELLULOSE FIBERS AND SLUDGES OR WASTE CONTAINING FAT AND/OR OIL.
DE8686906294T DE3683156D1 (en) 1985-10-16 1986-10-09 USE AS A FUEL FROM A MIXTURE OF CELLULOSE FIBERS AND FAT AND / OR OIL-CONTAINING SLAVES.
EP86906294A EP0252924B1 (en) 1985-10-16 1986-10-09 Use as fuel of a mixture of cellulosic fibres and fat-and/or oilcontaining sludges or waste materials
AU64797/86A AU6479786A (en) 1985-10-16 1986-10-09 Fuel consisting of a mixture of cellulosic fibres and fat- and/or oil containing sludges or waste materials
NO872438A NO170226C (en) 1985-10-16 1987-06-11 PROCEDURE FOR THE PREPARATION OF A FUEL COMPOSITION OF A MIXTURE OF CELLULOSE FIBERS AND FAT AND / OR OIL SLUES OR WASTE MATERIALS
FI872657A FI85873C (en) 1985-10-16 1987-06-15 BRAENSLE BESTAOENDE AV EN BLANDNING AV CELLULOSAFIBRER OCH FETT- OCH / ELLER OLJEHALTIGT SLAM ELLER AVFALLSMATERIAL.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DK472485A DK155835C (en) 1985-10-16 1985-10-16 PROCEDURE FOR THE FUEL PREPARATION CONSISTS OF A MIXTURE OF SOLID BIOMASS AND FAT AND / OR OIL SLUDGE CONCENTRATIONS
DK472485 1985-10-16

Publications (4)

Publication Number Publication Date
DK472485D0 DK472485D0 (en) 1985-10-16
DK472485A DK472485A (en) 1987-04-17
DK155835B true DK155835B (en) 1989-05-22
DK155835C DK155835C (en) 1989-11-13

Family

ID=8136131

Family Applications (1)

Application Number Title Priority Date Filing Date
DK472485A DK155835C (en) 1985-10-16 1985-10-16 PROCEDURE FOR THE FUEL PREPARATION CONSISTS OF A MIXTURE OF SOLID BIOMASS AND FAT AND / OR OIL SLUDGE CONCENTRATIONS

Country Status (10)

Country Link
EP (1) EP0252924B1 (en)
JP (1) JP2550333B2 (en)
AT (1) ATE70853T1 (en)
AU (1) AU6479786A (en)
BR (1) BR8606939A (en)
DE (1) DE3683156D1 (en)
DK (1) DK155835C (en)
FI (1) FI85873C (en)
NO (1) NO170226C (en)
WO (1) WO1987002377A1 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE521077C2 (en) * 2001-01-15 2003-09-30 Lars-Erik Mickelsson Solid fuel and process for its production
JP4727454B2 (en) * 2006-03-02 2011-07-20 太平洋セメント株式会社 Method for measuring waste tatami and method for producing solid fuel
CZ306752B6 (en) * 2010-05-14 2017-06-14 Česká zemědělská univerzita v Praze Fuel based on the residue from processing sugar sorghum
CN108893158A (en) * 2018-08-15 2018-11-27 河南东贵电子科技有限公司 A kind of manufacturing method of environment-friendly renewable coal

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR839271A (en) * 1938-06-14 1939-03-30 Process for manufacturing fuels from agricultural products in all forms: briquettes, pellets, etc.
DK60661C (en) * 1941-08-02 1943-03-08 Peter Adolf Nielsen Procedure for the manufacture of fuel briquettes.
US4052168A (en) 1976-01-12 1977-10-04 Edward Koppelman Process for upgrading lignitic-type coal as a fuel
JPS5413501A (en) * 1977-07-01 1979-02-01 Kayou Seishi Kk Method of producing solid fuels from waste liquid generated at reclaiming pulp in waste paper and oil paper
JPS5441901A (en) * 1977-09-09 1979-04-03 Yoichi Tsumura Method of manufacturing fuel by use of waste oil or the like
EP0035431A3 (en) * 1980-02-21 1981-12-16 Jean-Pierre Marcelot Process for manufacturing combustible pellets and devices for domestic and industrial use
EP0091532A1 (en) * 1982-04-08 1983-10-19 Ligi S.A. Process for the production of fuel from waste and recovery of the remaining materials
DK148119C (en) * 1982-10-29 1985-08-05 Niels Bendt Thagaard Hansen PROCEDURE TO USE IN THE MANUFACTURE OF PRESSED STRAWBERRIES FOR LINING PURPOSES
JPS60500294A (en) * 1982-12-30 1985-03-07 ダ−ビ−、ウィリアム・フレデリック Solid fuel and its manufacturing method
JPS60112893A (en) * 1983-11-23 1985-06-19 Kansai Sangyo Kk Apparatus for producing solid fuel from industrial waste
JPS6114200A (en) * 1984-06-29 1986-01-22 Nok Corp Manufacture of silicon nitride whisker

Also Published As

Publication number Publication date
FI872657A (en) 1987-06-15
WO1987002377A1 (en) 1987-04-23
BR8606939A (en) 1987-11-03
ATE70853T1 (en) 1992-01-15
EP0252924A1 (en) 1988-01-20
JPS63502752A (en) 1988-10-13
DK472485D0 (en) 1985-10-16
FI872657A0 (en) 1987-06-15
EP0252924B1 (en) 1991-12-27
FI85873B (en) 1992-02-28
DE3683156D1 (en) 1992-02-06
FI85873C (en) 1992-06-10
JP2550333B2 (en) 1996-11-06
AU6479786A (en) 1987-05-05
DK472485A (en) 1987-04-17
NO170226B (en) 1992-06-15
NO170226C (en) 1992-09-23
NO872438D0 (en) 1987-06-11
NO872438L (en) 1987-06-11
DK155835C (en) 1989-11-13

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